Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process

Recovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the...

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Main Authors: Mingming Yu, Shuya Pang, Guangjun Mei, Xiaodong Chen
Format: Article
Language:English
Published: MDPI AG 2016-10-01
Series:Minerals
Subjects:
Online Access:http://www.mdpi.com/2075-163X/6/4/109
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spelling doaj-3e75ca0083034212857ee35f82805be22020-11-24T21:51:47ZengMDPI AGMinerals2075-163X2016-10-016410910.3390/min6040109min6040109Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching ProcessMingming Yu0Shuya Pang1Guangjun Mei2Xiaodong Chen3School of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaSchool of Resources and Environmental Engineering, Wuhan University of Technology, Wuhan 430070, ChinaRecovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the majority of the impurities in the solution can be removed by adjusting the pH to 4.5 using a Na2S and NH3·H2O solution. Thirdly, the rare earths can be precipitated afterwards by adding a H2C2O4 solution and adjusting the pH to 2.0. Then rare earth oxides (REOs) can be obtained after calcining at 800 °C for 1 h. The characterization study of the waste phosphors and the rare earth oxide products was performed by XRD, XRF, and SEM-EDS analysis to determine the phase and morphological features. Influences of the factors, such as roasting temperatures and time, the addition of ammonium chloride on the roasting of waste phosphors, as well as the pH and the amount of oxalates on the precipitation of Y and Eu, were investigated. The maximum grade (99.84%) of mixed rare earth oxides and recovery rate (87.35%) of Y and Eu were obtained at the optimized conditions.http://www.mdpi.com/2075-163X/6/4/109waste phosphorschlorination roastingwater leachingrare earth elementsrecycling
collection DOAJ
language English
format Article
sources DOAJ
author Mingming Yu
Shuya Pang
Guangjun Mei
Xiaodong Chen
spellingShingle Mingming Yu
Shuya Pang
Guangjun Mei
Xiaodong Chen
Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
Minerals
waste phosphors
chlorination roasting
water leaching
rare earth elements
recycling
author_facet Mingming Yu
Shuya Pang
Guangjun Mei
Xiaodong Chen
author_sort Mingming Yu
title Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
title_short Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
title_full Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
title_fullStr Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
title_full_unstemmed Recovering Y and Eu from Waste Phosphors Using Chlorination Roasting—Water Leaching Process
title_sort recovering y and eu from waste phosphors using chlorination roasting—water leaching process
publisher MDPI AG
series Minerals
issn 2075-163X
publishDate 2016-10-01
description Recovering Y and Eu from waste phosphors using chlorination roasting followed by a water leaching process was investigated in this study. Firstly, by chlorination roasting and water leaching, Y and Eu elements present in waste phosphors were efficiently extracted into a leach solution. Secondly, the majority of the impurities in the solution can be removed by adjusting the pH to 4.5 using a Na2S and NH3·H2O solution. Thirdly, the rare earths can be precipitated afterwards by adding a H2C2O4 solution and adjusting the pH to 2.0. Then rare earth oxides (REOs) can be obtained after calcining at 800 °C for 1 h. The characterization study of the waste phosphors and the rare earth oxide products was performed by XRD, XRF, and SEM-EDS analysis to determine the phase and morphological features. Influences of the factors, such as roasting temperatures and time, the addition of ammonium chloride on the roasting of waste phosphors, as well as the pH and the amount of oxalates on the precipitation of Y and Eu, were investigated. The maximum grade (99.84%) of mixed rare earth oxides and recovery rate (87.35%) of Y and Eu were obtained at the optimized conditions.
topic waste phosphors
chlorination roasting
water leaching
rare earth elements
recycling
url http://www.mdpi.com/2075-163X/6/4/109
work_keys_str_mv AT mingmingyu recoveringyandeufromwastephosphorsusingchlorinationroastingwaterleachingprocess
AT shuyapang recoveringyandeufromwastephosphorsusingchlorinationroastingwaterleachingprocess
AT guangjunmei recoveringyandeufromwastephosphorsusingchlorinationroastingwaterleachingprocess
AT xiaodongchen recoveringyandeufromwastephosphorsusingchlorinationroastingwaterleachingprocess
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